Sourced conceptual inventory per tonne of blended FT liquid fuel from H2 and captured CO2: feeds, product and utility power from one open process simulation (König et al. 2015), burner flue gas and water from the element balance. Electrolysis and capture are outside. No flowsheet; not reviewed.
Fischer-Tropsch e-fuel from CO2 and hydrogen by reverse water-gas shift and cobalt FT synthesis
Sourced conceptual inventory per tonne of blended FT liquid fuel from H2 and captured CO2: feeds, product and utility power from one open process simulation (König et al. 2015), burner flue gas and water from the element balance. Electrolysis and capture are outside. No flowsheet; not reviewed.
Overview
- Capacity
- per tonne of FT liquid fuel (the dataset's basis); the source plant: 100 MW (LHV) of H2, 5.5 t/h fuel
What goes in and out
In
- HydrogenFeedstockfeed:H2: 3.01 t/h per 5.5 t/h fuel at 2.5 MPa; electrolytic hydrogen, supplier not chosen (lca/mappings.yaml)
- Carbon dioxideFeedstockfeed:CO2: 22.9 t/h per 5.5 t/h fuel at 0.1 MPa; captured CO2, taken as from a fossil point source (ASSUMED), supplier not chosen
Out
- Fischer-Tropsch liquid fuelMain product
- WastewaterWastereaction water, closes the source's mass balance
Utilities: Electricity (plant utilities only; the electrolyser's power is in the hydrogen)
Life cycle assessment
No footprint assessed yet; the process is part of the life-cycle inventory below.
In the open LCI database (cheme-as-code-atlas-preview-a3c52e4) as Fischer-Tropsch liquid fuel (gasoline, kerosene and diesel cuts, not fractionated) Preliminary.
Download it for Brightway, openLCA and other tools.
In the LCI database: system model, datasets and KPIs against the benchmarks
In the LCI database
- Status
- Preliminary 2 unmapped exchanges. Some exchanges have no background mapping yet: they are exported unlinked and count no burden, so the inventory is incomplete.
- System model
- attributional, cut-off (methodology 1.1.0)
- Allocation
- mass (single-output, from default) · product:fischer-tropsch-fuel 100 %
- Allocation findings
- none
- Change report
- Not available: this build has no change report against an earlier release.
- Dataset pages
- Fischer-Tropsch liquid fuel (gasoline, kerosene and diesel cuts, not fractionated) Preliminary
KPI benchmark positions
| KPI | Value | Reference range | Position |
|---|---|---|---|
| Share of the CO2 carbon fed that ends in the liquid fuel | – kg/kg | 0.455 to 0.455 kg/kg | not evaluated |
| Liquid fuel LHV per LHV of the hydrogen fed | – MJ/MJ | 0.582 to 0.582 MJ/MJ | not evaluated |
| CO2 fed per t of Fischer-Tropsch liquid fuel | – t/t | 6.81 to 6.81 t/t | not evaluated |
| Electricity used by the synthesis plant per t of FT liquid fuel (electrolysis excluded) | – kWh/t | 1,369 to 1,369 kWh/t | not evaluated |
Maturity and review
Design maturity Concept (claimed): An idea or first flowsheet; numbers are rough. No independent engineering review yet. Automated checks passing is not a review.
Calculation maturity, from the checked evidenceNot assessed
The process has no maturity report (cheme maturity, checks/maturity.json), so no calculation maturity is established.
cheme maturity --write.Artifact completeness
Which deliverables exist. They never raise a calculation maturity level: a drawing from unchecked numbers is still unchecked.
Not reported without a maturity report.
Independent review
Not independently reviewed
No independent engineering review yet. Automated checks passing is not a review.
Set by people only. Reaching a calculation maturity level or passing automated checks is not an independent review or an approval.
Where the evidence comes from
- Report
processes/e-fuels-1/checks/maturity.json(not in the library)- Method
- How ChemE-as-Code checks the levels (requirement by requirement)
Open items
0 open items · 0 closed
New action itemNew engineering holdNew technical queryNew design changeAll issues
Sources
- Library version
- a3c52e4 (process last changed in a3c52e4)
- Data
- Catalog record (JSON) · CC-BY-4.0
- Files
- View the files on GitHub · change history and authors
References
- König, D.H., Baucks, N., Dietrich, R.-U., Wörner, A. (2015) Simulation and evaluation of a process concept for the generation of synthetic fuel from CO2 and H2. Energy 91:833-841 (accepted manuscript in DLR elib, https://elib.dlr.de/98357/) · doi:10.1016/j.energy.2015.08.099
- Zang, G., Sun, P., Elgowainy, A., Bafana, A., Wang, M. (2021) Life cycle analysis of electrofuels: Fischer-Tropsch fuel production from hydrogen and corn ethanol byproduct CO2. Environ. Sci. Technol. 55:3888-3897 (DOE public-access copy, OSTI 1807679); benchmarks only · doi:10.1021/acs.est.0c05893
How to cite
For the data, cite the Process Atlas paper; for the platform that builds and checks it, the ChemE-as-Code paper.
Schweidtmann, A. M. & Weber, J. M. (2026, in preparation). Process Atlas: an open, git-native, reproducible library and life cycle inventory of chemical processes (working title).
For this process: "Fischer-Tropsch e-fuel from CO2 and hydrogen by reverse water-gas shift and cobalt FT synthesis", ChemE-as-Code process library, version a3c52e4.
BibTeX
@unpublished{schweidtmann_process_atlas,
author = {Schweidtmann, Artur M. and Weber, Jana M.},
title = {{Process Atlas: an open, git-native, reproducible library and life cycle inventory of chemical processes (working title)}},
year = {2026},
url = {https://atlas.cheme-as-code.org},
note = {in preparation}
}Schweidtmann, A. M. (2026). ChemE-as-Code: An Open-Source Platform for Agentic AI in Chemical Engineering. arXiv:2611.07947. https://doi.org/10.48550/arXiv.2611.07947
BibTeX
@misc{schweidtmann_cheme_as_code,
author = {Schweidtmann, Artur M.},
title = {{ChemE-as-Code: An Open-Source Platform for Agentic AI in Chemical Engineering}},
year = {2026},
eprint = {2611.07947},
archivePrefix = {arXiv},
doi = {10.48550/arXiv.2611.07947},
url = {https://arxiv.org/abs/2611.07947}
}